超临界甲烷在竖直圆管内加热的数值模拟
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国家自然科学基金资助项目(51476102)


Numerical Simulation on Supercritical Methane in a Heating Vertical Circular Tube
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    摘要:

    在超临界压力下甲烷的相变现象消失,并且物性变化非常剧烈,换热过程变得相当复杂.通过数值模拟软件FLUENT导入制冷剂物性软件REFPROP中超临界甲烷的材料模型,在准确反映超临界甲烷的热力性能和传输物性变化的情况下,采用数值模拟的方法对竖直加热圆管内超临界压力下甲烷的传热特性进行了研究.在分析不同工况下超临界甲烷换热情况的基础上,重点研究了浮升力对换热的影响,并得出了适用于甲烷的浮升力影响判别标准.结果表明:换热系数随着压力的减小而增加;当流体平均温度接近临界温度,壁面温度大于临界温度时有利于换热;在高热流密度,低质量流量的条件下容易造成传热恶化;浮升力改变了径向速度分布曲线,抑制了湍动能的产生,削弱了换热.

    Abstract:

    The physical properties of methane change drastically and the phenomenon of phase change vanishes under supercritical pressure, so the heat exchange process is extremely complex. The heat transfer characteristics of supercritical methane in a heating vertical circular tube were investigated numerically. The thermal performance and transport properties of supercritical methane were obtained by introducing the material model of methane in the refrigerant properties software REFPROP. The results show that it is advantageous to the heat transfer when the averaged fluid temperature is close to the critical temperature and the wall temperature is higher than the critical temperature. And the heat transfer coefficient increases with the decrease of pressure. High heat flux and low mass flow rate will cause the deterioration of heat transfer. Then the influence of buoyancy on the heat transfer was studied carefully and the buoyancy judgment standard suitable for methane was obtained. It is found that the buoyancy which changes the distribution of radial velocity and inhibits the generation of turbulent kinetic energy weakens the convective heat transfer.

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郭占魁,忻晔晨,李凌.超临界甲烷在竖直圆管内加热的数值模拟[J].上海理工大学学报,2017,39(1):30-34,57.

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  • 收稿日期:2016-10-17
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  • 在线发布日期: 2017-03-20
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